Non-isothermal thermogravimetric kinetic analysis of the thermochemical conversion of human faeces

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dc.contributor.author Fidalgo, Beatriz
dc.contributor.author Chilmeran, M.
dc.contributor.author Somorin, Tosin Onabanjo
dc.contributor.author Sowale, Ayodeji
dc.contributor.author Kolios, Athanasios
dc.contributor.author Parker, Alison
dc.contributor.author Williams, Leon
dc.contributor.author Collins, Matt
dc.contributor.author McAdam, Ewan J.
dc.contributor.author Tyrrel, Sean F.
dc.date.accessioned 2018-09-10T15:27:05Z
dc.date.available 2018-09-10T15:27:05Z
dc.date.issued 2018-08-29
dc.identifier.citation Beatriz Fidalgo, M. Chilmeran, Tosin Somorin, et al., Non-isothermal thermogravimetric kinetic analysis of the thermochemical conversion of human faeces. Renewable Energy, Volume 132, March 2019, Pages 1177-1184 en_UK
dc.identifier.issn 0960-1481
dc.identifier.uri https://doi.org/10.1016/j.renene.2018.08.090
dc.identifier.uri http://dspace.lib.cranfield.ac.uk/handle/1826/13472
dc.description.abstract The “Reinvent the Toilet Challenge” set by the Bill & Melinda Gates Foundation aims to bring access to adequate sanitary systems to billions of people. In response to this challenge, on-site sanitation systems are proposed and being developed globally. These systems require in-situ thermal treatment, processes that are not well understood for human faeces (HF). Thermogravimetric analysis has been used to investigate the pyrolysis, gasification and combustion of HF. The results are compared to the thermal behaviour of simulant faeces (SF) and woody biomass (WB), along with the blends of HF and WB. Kinetic analysis was conducted using non-isothermal kinetics model-free methods, and the thermogravimetric data obtained for the combustion of HF, SS and WB. The results show that the devolatilisation of HF requires higher temperatures and rates are slower those of WB. Minimum temperatures of 475 K are required for fuel ignition. HF and SF showed similar thermal behaviour under pyrolysis, but not under combustion conditions. The activation energy for HF is 157.4 kJ/mol, relatively higher than SS and WB. Reaction order for HF is lower (n = 0.4) to WB (n = 0.6). In-situ treatment of HF in on-site sanitary systems can be designed for slow progressive burn. en_UK
dc.language.iso en en_UK
dc.publisher Elsevier en_UK
dc.rights Attribution 4.0 International *
dc.rights.uri http://creativecommons.org/licenses/by/4.0/ *
dc.subject Pyrolysis en_UK
dc.subject Combustion en_UK
dc.subject Thermogravimetric analysis en_UK
dc.subject Kinetics en_UK
dc.subject Human faeces en_UK
dc.subject Nano membrane toilet en_UK
dc.title Non-isothermal thermogravimetric kinetic analysis of the thermochemical conversion of human faeces en_UK
dc.type Article en_UK


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